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A method for selectively leaching and separating vanadium and iron from stone coal vanadium ore

A stone coal vanadium and selectivity technology, applied in the direction of improving process efficiency, can solve the problems of incomplete separation of vanadium and iron, the leaching rate of vanadium needs to be improved, and increase energy consumption, so as to reduce the difficulty of subsequent impurity removal, iron vanadium High separation efficiency and reduced leaching difficulty

Active Publication Date: 2021-02-05
INST OF PROCESS ENG CHINESE ACAD OF SCI
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, ion exchange is usually used to treat leachate containing pentavalent vanadium, and the pH of the leachate is required to be not lower than 2.0 for better ion exchange. However, when the pH of the leachate reaches above 1.5, it can slowly precipitate vanadium-containing precipitates, resulting in vanadium loss
The solvent extraction method is suitable for vanadium-containing leaching solution with many impurities and high acidity. CN 103695643A discloses a method for extracting vanadium pentoxide from stone coal vanadium ore mixed with acid heap ore. In the method, the stone coal vanadium ore is crushed and mixed with acid Deposit, stockpile mines are leached with clean water, the leachate and leaching slag filtered by the pulp, the leachate is neutralized by lime and soda ash, then extracted with the extractant, back-extracted with sulfuric acid, and then prepared from the back-extraction liquid through a series of operations to prepare vanadium pentoxide, but While this method realizes the separation of vanadium and iron and the enrichment of vanadium, a small part of iron and vanadium will still be co-extracted, which will affect the quality of subsequent vanadium products.
The chemical precipitation method refers to the selective oxidation of iron in the leachate to ferric iron by selecting a suitable oxidant under certain conditions, and then the separation of vanadium and iron is achieved by chemical precipitation, but the selective oxidation of iron is difficult to accurately control , often resulting in higher vanadium loss
[0005] In addition, in order to improve the incomplete separation of vanadium and iron in the vanadium-containing leaching solution and the high loss of vanadium, CN106755959A discloses a method for the two-stage selective leaching of stone coal to separate vanadium and iron. Roasting in an oxidative atmosphere to obtain a roasted material, the roasted material was pickled with sulfuric acid solution I and sulfuric acid solution II to obtain iron-containing leachate and vanadium-containing leachate, but the roasting temperature (800-900°C) of this method is relatively high, which increases the Its energy consumption, sulfur, nitrogen and other elements contained in stone coal will generate sulfur and nitrogen-containing polluting gases during the roasting process, and the leaching rate of vanadium still needs to be improved

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  • A method for selectively leaching and separating vanadium and iron from stone coal vanadium ore

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Embodiment 1

[0061] This embodiment provides a method for selectively leaching and separating vanadium and iron from stone coal vanadium ore, the process flow diagram of the method is as follows figure 1 shown, including the following steps:

[0062] (1) The stone coal vanadium ore is crushed and ball milled to obtain a stone coal vanadium ore powder with a particle size of 80 meshes. The mineral powder is mixed with dilute sulfuric acid with a concentration of 20wt% and then leached once. The solid ratio is 1.5mL / g, the temperature is 90°C, and the time is 1h, and the first leachate and the first leach residue are obtained by filtration;

[0063] (2) add dilute sulfuric acid to the first leaching solution that step (1) obtains in time for recycling, then add iron powder, and Fe 3+ reduced to Fe 2+ Post-cooling and crystallization to recover FeSO 4 ·7H 2 O crystals, the cooling crystallization temperature is 5°C, and the remaining crystallization mother liquor is used for vanadium reco...

Embodiment 2

[0069] This embodiment provides a method for selectively leaching and separating vanadium and iron from stone coal vanadium ore, said method comprising the following steps:

[0070] (1) Crushing and ball milling the stone coal vanadium ore to obtain the stone coal vanadium ore ore powder with a particle size of 120 meshes. The ore powder is mixed with dilute sulfuric acid with a concentration of 10wt% and then leached once. The solid ratio is 6mL / g, the temperature is 60°C, and the time is 3h, and the first leaching solution and the first leaching residue are obtained by filtration;

[0071] (2) add dilute sulfuric acid to the first leaching solution that step (1) obtains in time for recycling, then add potassium thiosulfate, and Fe 3+ reduced to Fe 2+ Post-cooling and crystallization to recover FeSO 4 ·7H 2 O crystals, the cooling crystallization temperature is 10°C, and the remaining crystallization mother liquor is used for vanadium recovery;

[0072] (3) Mix the first ...

Embodiment 3

[0077] This embodiment provides a method for selectively leaching and separating vanadium and iron from stone coal vanadium ore, said method comprising the following steps:

[0078] (1) The stone coal vanadium ore is crushed and ball milled to obtain a stone coal vanadium ore powder with a particle size of 40 meshes. The mineral powder is mixed with dilute sulfuric acid with a concentration of 30wt% and then leached once. The solid ratio is 1mL / g, the temperature is 20°C, and the time is 10h, and the first leaching solution and the first leaching residue are obtained by filtration;

[0079] (2) add dilute sulfuric acid to the first leaching solution that step (1) obtains in time for recycling, then add sodium thiosulfate, and Fe 3+ reduced to Fe 2+ Post-cooling and crystallization to recover FeSO 4 ·7H 2 O crystal, the temperature of cooling and crystallization is 15°C, and the remaining crystallization mother liquor is used for recovery of vanadium;

[0080] (3) Mix the f...

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Abstract

The invention provides a method for selectively leaching and separating vanadium and iron from stone coal vanadium ore. and the first leaching slag; adding a reducing agent after the obtained first leachate is recycled, and after the reaction is cooled and crystallized to recover the ferrous salt; the obtained first leaching slag is mixed with concentrated sulfuric acid and then matured to obtain a clinker; the obtained The slag is added with water for secondary leaching, and the second leaching solution and the second leaching residue are obtained by solid-liquid separation. The method adopts a two-stage leaching process to selectively leaching iron and vanadium, which prevents a large amount of impurity elements such as iron in the stone coal vanadium ore from entering the vanadium-containing solution from the source, reduces the concentration of impurity ions in the vanadium-containing leaching solution, and improves the subsequent content of the leaching solution. The purification efficiency of the vanadium solution; the method is simple to operate, does not require roasting, is environmentally friendly, has less acid consumption, lower cost and higher economic benefits.

Description

technical field [0001] The invention belongs to the technical field of nonferrous metal extraction, and relates to a method for selectively leaching and separating vanadium and iron from stone coal vanadium ore. Background technique [0002] Stone coal vanadium ore is an important vanadium resource with abundant reserves, and the vanadium contained therein (expressed as V 2 o 5 Count) up to 1.18×10 8 t, accounting for about 87% of the national vanadium reserves. According to the degree of weathering, stone coal can be divided into oxidized stone coal vanadium ore and primary stone coal vanadium ore. Vanadium in oxidized stone coal vanadium ore exists in the form of tetravalent vanadium or pentavalent vanadium, which is in the free state of oxides. , so it is easy to extract by acid leaching; while the vanadium in primary stone coal vanadium ore exists in the lattice structure of aluminosilicate in the form of trivalent vanadium, which has strong stability and is difficult...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B3/08C22B3/44C22B34/22
CPCC22B3/08C22B3/44C22B34/22Y02P10/20
Inventor 刘宏辉董玉明杨建旺裴丽丽王明华徐红彬张懿
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI
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